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Select form type to navigate to the emission calculator for the source type:
Company Name: Note: Don't forget to enable macros.
Insert Company and/or site name here.
Choose form type:
Blodon and/or process vents !hroughout this or"boo":
Boilers and #eaters $Input variables into the blue bo%es.
Compressor engines $&missions ill be in the green bo%es.
lares
rac tan"s
(lycol dehydrators !o be notified of any updates to this or"boo"
)oading
*iping component fugitive areas
Separators
Condensate storage tan"s
Crude oil storage !an"s
*roduced ater storage tan"s
!urbines
+ther:
Non,flare combustive device
◊ Emitted 1 ton or more of volatile organic compounds (VOC), or
◊ Emitted 01 tons per year or more of a ha!ardous air pollutant ("#$)
◊ less than % tons of &O',
◊ less than % tons of VOC, and
◊ less than 1 ton of aggregate "#$s
The Barnett Shale Special Inventory list server hamessages about the agency’s special inventory ef
If you haven't already done so, we recommend yto receive any important updates concerning the iemission calculator. To do so, you will need to crTC!’s distribution service, "ov#elivery.com, smanage your subscriptions. To create a profile osubscriptions, please visit$ http$%%service.govdelivcodeT(TC!.
Complete a form for each piece of euipment (listed aove) that meets one of thefollo*ing criteria for +00:
◊ Emitted 1 ton or more of &O',
-f individual pieces of euipment do not meet the reuirements listed aove, theymay e omitted from the inventory provided that the total emissions from all suchunreported sources are:
-f the total emissions from the omitted pieces of euipment do not satisfy thesereuirements, report each source starting *ith the piece of euipment *ith thehighest emissions until the total emissions of the remaining omitted sourcessatisfy the aove reuirements
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Barnett Shale *hase II Identification Information: $Input variables into the b
Company Name: Insert Company and/or site name here. $&missions ill be in the g
Blodon -:
mole . *eight .
(as nalysis: &itrogen +/01/ 0 23-V405
00% 0 23-V405 VO
0/1// 0 23-V405 VOC *eig
methane (C1) 180+8 0 23-V405
ethane (C+) 0080 0 23-V405
propane (C) 0%8+ 0 23-V405 "#$ content of g
i9utane (C) %/1+++ 0 23-V405 en!en
n9utane (C) %/1+++ 0 23-V405 ;oluen
i9pentane (C%)
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#eater and Boiler &mission Calculations 0fueled by natural gas1
Barnett Shale *hase II Identification Information: $Input variables into the b
Company Name: Insert Company and/or site name here. $&missions ill be in the
#eater or Boiler -:
"eater4oiler rating (@@tu4hr):
pick from list
Operating hours4year:
uel "eat Value (tu4BC):
pollutant emission factor (l4@@C)? tpy
VOC %% 23-V405
2 23-V405
? Emission actors from #$9+, Chapter 1, ;ales 191 and 19+
Company's 5ni7ue IdentificationNumber:
6ating aove is 0select from list1:
&O=
Back to Workbook N
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&ngine &mission Calculations 0fueled by natural gas1
Barnett Shale *hase II Identification Information:
Company Name: Insert Company and/or site name here. $
&ngine -: $
N
#orsepoer: !
uel consumption 0Btu/hp,hr1:9.
#ours of operation per year:
pick from list .
&ngine )oad: pick from list
units
+C 2.2 2.2 lb/44Btu 2.2222
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lare
Barnett Shale *hase II Identification Information:
Company Name: Insert Company and/or site name here.
lare -:
(eneral Information &missioEmissio
non9steam assisted flare *ith high tu stream flared
Emission actors for aste Das Btream(s) (l4@@tu)
01/
Ies
Emission actors for $ilot Btream (l4@@scf)
100
&o
Enter !eros into the o'es in the column for Btream &o + elo*
Emission actors for #dded uel Btream (l4@@tu)
0
/
Stream Information
Stream Sent to lare No. 9 < ; ? >
$ilot(s) e': oil tanJ e': *ater tanJ
Company's 5ni7ueIdentification Number:
091 Fhat type of flare is
thisG *ic" from list.
&O'
0
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rac Storage !an"
Barnett Shale *hase II Identification Information:
Company Name: Insert Company and/or site name here.
rac !an"-:
!an" emissions are made up of different components6 or"ing6 breathing and fl
5sing &* !NJS ;.2 Softare to calculate For"ing and Breathing losses
For"ing and Breathing )osses
E$# ;#&MB 0This softare is a!aila"le for donload at .epa.#o!$ttn$chief$softare$tanks$inde%.html
orJing reathing
VOCs, C>
en!ene
;oluene
E en!ene
=ylenes
n9he'ane+,+, 9 ;rimethylpentane
#ny #dditional "#$ (if applicale):
5sing &K* !NJS ;.2 Softare to calculate For"ing and Breathing losses
This softare can "e purchased from .#lo"al.ihs.com
Component Controlled Emissions Nton4yr
VOCs, C>
en!ene
;oluene
E en!ene
=ylenes
n9C8
++;rimethylp
Company's 5ni7ueIdentification Number:
EP$ ;anJs (accounts for *orJing, reathing and flash losses)
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Notes:
$ &nter variables into blue bo%es
$ &missions ill be in green bo%es
ash losses.
lash losses !otal &missions
3irect @easurement of Emissions
$rocess Bimulator @odels
lash losses
VOCs, C> VOCs, C> 00000
en!ene en!ene 00000
;oluene ;oluene 00000
E en!ene E en!ene 00000
=ylenes =ylenes 00000
n9he'ane n9C8 00000+,+, 9 ;rimethylpentane +,+, 9 ;rimethylpentane 00000
#ny #dditional "#$ (if applicale): #ny #dditional "#$ (if applicale):
00000
00000
00000
00000
#nnual Emissions tons per year
VOCs, C> 00000
en!ene 00000
;oluene 00000
E en!ene 00000
=ylenes 00000
n9C8 00000
+,+, 9 ;rimethylpentane 00000
Valid @ethods for Condensate (Qse one of thefollo*ing accepted methods):
the gas4oil ratio (DO6) method
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6eport VOC emissions onrac ;anJ(s) ;a
6eport "#$ emissions on
rac ;anJ(s) ta or "#$speciation ta if the valuesare greater than or eualto 01 tpy
6eport VOC emissions onrac ;anJ(s) ;a
6eport "#$ emissions onrac ;anJ(s) ta or "#$speciation ta if the valuesare greater than or eualto 01 tpy
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(lycol Dehydrator &mission Calculations
Company Name: Insert Company and/or site name here.
Still-:
Company's 5ni7ue Identification Number:
;here are t*o options that are used most commonly to determine the emissions from a glycol dehydr
$lease chose the option you prefer:
(I,()HCalc *rogram6un the soft*are program maJing sure to using a *et gas analysis for your input ;his analysis shou
5ncontrolled/ Controlled egenerator &missions lash (as &m
Component tpy Component
$ropane $ropane
-soutane -soutane
n9utane n9utane
-sopentane -sopentanen9pentane n9pentane
cyclopentane cyclopentane
n9he'ane n9he'ane
cyclohe'ane cyclohe'ane
other he'anes other he'anes
heptanes heptanes
methylcyclohe'ane methylcyclohe'ane
+,+, ;rimethylpentane +,+, ;rimethylpentane
en!ene en!ene
;oluene ;oluene
Ethylen!ene Ethylen!ene
=ylene(s) =ylene(s)C/> "eavies C/> "eavies
;otal VOC ;otal VOC
ich/)ean nalysis
R D6-9DAICalc Boft*are $rogram
R 6ich4Aean #nalysis
;he total emissions for a glycol dehydrator should include oth the KControlled 6egenerator Emissionpresent and if the flash tanJ is not 100. controlled *ith the recycled4recompression option) y revie
emissionsClicJ to see e'ample reports:
Controlled regenerator *ith flash tanJ
Qncontrolled regenerator *ith flash tanJ
Qncontrolled regenerator vent *ith a flash tanJ *ith recycle4recompressi
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Dlycol recirculation rate (gal4min)
#nnual hour of operation (hr)
Component ich 0mg/)1 )ean 0mg/)1 tpy
;otal VOC 000n9he'ane 000
+,+, ;rimethylpentane 000
en!ene 000
;oluene 000
Ethylen!ene 000
=ylene(s) 000
#dditional "#$s
000
000
000
000
Euation used in 6ich4Aean #nalysis:
here:
t 7 annual hours of operation
5sing a laboratory analysis of enriched and lean glycol samples that includes benAene6 toluefolloing information.
(Crich
9 Clean
) ? Hrecirc
? t ?
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Notes:
$ &nter variables into blue bo%es
$ &missions ill be in green bo%es
$ Instructions for using this form.
ator
ld include an e'tended gas analysis that includes ut not limited to ;E=
issions !otal (lycol Still &missions
tpy Component tpy
;otal VOC 0
en!ene 0
;oluene 0
Ethylen!ene 0=ylene(s) 0
+,+, ;rimethylpentane 0
n9he'ane 0
sK or KQncontrolled 6egenerator EmissionsK and the Klash Das EmissionsK (if the flash tanJ is*ing the D6-9DAICalc #ggregate Calculations report you *ill e ale to determine your total
n option
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e6 ethylbenAene and %ylene0s16 complete the
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Calculations
n Information: Notes:
Insert Company and/or site name here. $ &nter va
$ &missio
$ 5se thes
0completion is optional1
;?=.> 2
0 1
0 1
0 1
0 1
0 1
0 1
0 1
0 1
0 1
0 1
0 1
0 1
0 1
tpy
00000 6eport VOC emissions on KAoadingK ;a
00000
00000
00000
00000
00000
00000
00000 eport any dditional #*s if they are greater than or e7ual to 2.9 tpy.00000
Can assume /
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ugitives &mission Calculations
Complete this form for each type of each stream type.
Barnett Shale *hase II Identification Information: Notes:
Company Name: Insert Company and/or site name here. $Input variables int
ugitive rea -: $&missions ill be
(as nalysis:
mole . *eight .
&itrogen +/01/ 0 23-V405 VO
00% 0 23-V405 VOC
0/1// 0 23-V405 VOC *eig
methane (C1) 180+8 0 23-V405
ethane (C+) 0080 0 23-V405
propane (C) 0%8+ 0 23-V405 "#$ content of
i9utane (C) %/1+++ 0 23-V405 en!ene
n9utane (C) %/1+++ 0 23-V405 ;oluenei9pentane (C%)
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'ylenes (@, $, O) 10818 0 23-V405
undecanes (C11>)? 1%81 0 23-V405
;O;#AB: 00000 0 23-V405
? -f the @olecular eight is availale on the gas analysis, enter it aove, other*ise, can use the default value
ugitives &mission Calculations
$lease choose from the follo*ing:
(as (as
numer component l4hr tpy
Valve 000% 000+ 0 0 23-V405
$ump Beal 000+ 000%+ 0 0 23-V405
Connector 0000+ 0000 0 0 23-V405
lange 0000 0000/8 0 0 23-V405
Open9ended Aine 000+ 0001 0 0 23-V405
Other 000// 0010 0 0 23-V405
;otal: 0 0
)ight +il )ight +il
numer component l4hr tpy
Valve 000+% 000%%1 0 0 23-V405
$ump Beal 001 00+/88 0 0 23-V405
Connector 0000+1 00008 0 0 23-V405
lange 000011 0000+ 0 0 23-V405
Open9ended Aine 0001 0000 0 0 23-V405
Other 000
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;oluene 23-V405
Ethylen!ene 23-V405
=ylene(s) 23-V405
n9"e'ane 23-V405
? or fugitive calculations, VOC content should e VOC content of total hydrocarons, not of total sample
6eport en!ene, Ethylen!ene, ;oluene,=ylene, and n9he'ane on the $hase --calculator if they are greater than 01 tpy onthe Kugitive(s)K ta
Emission factors are for oil and gas production facilities (not refineries), and come from the E$#Ss K$rotocol for Euipment AeaJ Emission Estimate69%901
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+C en!ene ;oluene Ethylen!ene =ylene n9he'ane
tpy tpy tpy tpy tpy tpy
23-V405 23-V405 23-V405 23-V405 23-V405 23-V405
23-V405 23-V405 23-V405 23-V405 23-V405 23-V405
23-V405 23-V405 23-V405 23-V405 23-V405 23-V405
23-V405 23-V405 23-V405 23-V405 23-V405 23-V405
23-V405 23-V405 23-V405 23-V405 23-V405 23-V405
23-V405 23-V405 23-V405 23-V405 23-V405 23-V405
23-V405 23-V405 23-V405 23-V405 23-V405 23-V405
tpy tpy tpy tpy tpy tpy
23-V405 23-V405 23-V405 23-V405 23-V405 23-V405
23-V405 23-V405 23-V405 23-V405 23-V405 23-V405
23-V405 23-V405 23-V405 23-V405 23-V405 23-V405
23-V405 23-V405 23-V405 23-V405 23-V405 23-V405
23-V405 23-V405 23-V405 23-V405 23-V405 23-V405
23-V405 23-V405 23-V405 23-V405 23-V405 23-V405
23-V405 23-V405 23-V405 23-V405 23-V405 23-V405
tpy tpy tpy tpy tpy tpy
0000 0000 0000 0000 0000 0000
0000 0000 0000 0000 0000 00000000 0000 0000 0000 0000 0000
0000 0000 0000 0000 0000 0000
0000 0000 0000 0000 0000 0000
0000 0000 0000 0000 0000 0000
0 0 0 0 0 0
tpy tpy tpy tpy tpy tpy
0000 0000 0000 0000 0000 0000
0000 0000 0000 0000 0000 0000
0000 0000 0000 0000 0000 0000
0000 0000 0000 0000 0000 0000
0000 0000 0000 0000 0000 0000
0000 0000 0000 0000 0000 0000
0000 0000 0000 0000 0000 0000
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&N!&D S&*!+ &4ISSI+N C)C5)!I+N
Barnett Shale *hase II Identification Information: $Input variables into the
Company Name: Insert Company and/or site name here. $&missions ill be in the
Separators -:
(as nalysis of separator vent gas:
mole . *eight .
&itrogen +/01/ 0 23-V405 VOC
CO+ 00% 0 23-V405 V
"+B 0/1// 0 23-V405 VOC *e
methane (C1) 180+8 0 23-V405
ethane (C+) 0080 0 23-V405
propane (C) 0%8+ 0 23-V405 "#$ content of
i9utane (C) %/1+++ 0 23-V405 en!e
n9utane (C) %/1+++ 0 23-V405 ;oluei9pentane (C%)
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Condensate Storage !an"
Barnett Shale *hase II Identification Information:
Company Name: Insert Company and/or site name here.
Condensate !an"-:
!an" emissions are made up of different components6 or"ing6 breathing and fl
5sing &* !NJS ;.2 Softare to calculate For"ing and Breathing losses
For"ing and Breathing )osses
E$# ;#&MB 0
This softare is a!aila"le for donload at .epa.#o!$ttn$chief$softare$tanks$inde%.html
orJing reathing
VOCs, C>
en!ene
;oluene
E en!ene
=ylenes
n9he'ane+,+, 9 ;rimethylpentane
#ny #dditional "#$ (if applicale):
5sing &K* !NJS ;.2 Softare to calculate For"ing and Breathing losses
This softare can "e purchased from .#lo"al.ihs.com
Component Controlled Emissions Nton4yr
VOCs, C>
en!ene
;oluene
E en!ene
=ylenes
n9C8
++;rimethylp
Das condensate is defined as a liuid hydrocaron *ith an #$- gravity greater than 0° at 80° (a
Company's 5ni7ueIdentification Number:
EP$ ;anJs (accounts for *orJing, reathing and flash losses)
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Notes:
$ &nter variables into blue bo%es
$ &missions ill be in green bo%es
ash losses.
lash losses !otal &missions
3irect @easurement of Emissions$rocess Bimulator @odels
lash losses
VOCs, C> VOCs, C>
en!ene en!ene
;oluene ;oluene
E en!ene E en!ene
=ylenes =ylenes
n9he'ane n9C8+,+, 9 ;rimethylpentane +,+, 9 ;rimethylpentane
#ny #dditional "#$ (if applicale): #ny #dditional "#$ (if app
#nnual Emissions
VOCs, C>
en!ene
;oluene
E en!ene
=ylenes
n9C8
+,+, 9 ;rimethylpentane
nd a specific gravity less than 0/+%+)
Valid @ethods for Condensate (Qse one of the follo*ingaccepted methods):
the gas4oil ratio (DO6) method
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00000
00000
00000
00000
00000
0000000000
licale):
00000
00000
00000
00000
tons per year
00000
00000
00000
00000
00000
00000
00000
6eport VOC emissions onCondensate ;anJ(s) ;a
6eport "#$ emissions onCondensate ;anJ(s) ta or
"#$ speciation ta if thevalues are greater than oreual to 01 tpy
6eport VOC emissions onCondensate ;anJ(s) ;a
6eport "#$ emissions onCondensate ;anJ(s) ta or"#$ speciation ta if thevalues are greater than oreual to 01 tpy
gation
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Crude +il Storage !an"
Barnett Shale *hase II Identification Information:
Company Name: Insert Company and/or site name here.
Crude +il !an"-:
!an" emissions are made up of different components6 or"ing6 breathing and flash l
5sing &* !NJS ;.2 Softare to calculate For"ing and Breathing losses
For"ing and Breathing )osses
E$# ;#&MB 0This softare is a!aila"le for donload at .epa.#o!$ttn$chief$softare$tanks$inde%.html
orJing reathing
VOCs, C>
en!ene
;oluene
E en!ene
=ylenes
n9he'ane
+,+, 9 ;rimethylpentane
#ny #dditional "#$ (if applicale):
5sing &K* !NJS ;.2 Softare to calculate For"ing and Breathing losses
This softare can "e purchased from .#lo"al.ihs.com
Component Controlled Emissions Nton4yr
VOCs, C>
en!ene
;oluene
E en!ene
=ylenes
Crude oil is defined as heavy, lo* volatility oil appro'imated y a DO6 less than 1,
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n9C8
++;rimethylp
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Notes:
$ &nter variables into blue bo%es
$ &missions ill be in green bo%es
sses.
lash losses !otal &missions
3irect @easurement of Emissions
$rocess Bimulator @odels
6ollins, @cCain, and Creeger correlations
lash losses
VOCs, C> VOCs, C>
en!ene en!ene
;oluene ;oluene
E en!ene E en!ene
=ylenes =ylenes
n9he'ane n9C8
+,+, 9 ;rimethylpentane +,+, 9 ;rimethylpentane
#ny #dditional "#$ (if applicale): #ny #dditional "#$ (if app
#nnual Emissions
VOCs, C>
en!ene
;oluene
E en!ene
=ylenes
arrel and an #$- gravity less than 0°
Valid @ethods for Crude Oil (Qse one of the follo*ing
accepted methods):
Vasue!9eggs correlation
the gas4oil ratio (DO6) method
Back to Wo
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n9C8
+,+, 9 ;rimethylpentane
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00000
00000
00000
00000
00000
00000
00000
licale):
00000
00000
00000
00000
tons per year
00000
00000
00000
00000
00000
6eport VOC emissions on CrudeOil ;anJ(s) ;a
6eport "#$ emissions on CrudeOil ;anJ(s) ta or "#$ speciationta if the values are greater thanor eual to 01 tpy
6eport VOC emissions on CrudeOil ;anJ(s) ;a
6eport "#$ emissions on CrudeOil ;anJ(s) ta or "#$ speciationta if the values are greater than
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*roduced Fater Storage !an"
Barnett Shale *hase II Identification Information:
Company Name: Insert Company and/or site name here.
*roduced Fater !an"-:
Company's 5ni7ue Identification Number:
!an" emissions are made up of different components6 or"ing6 breathing and fl
5sing &* !NJS ;.2 Softare to calculate For"ing and Breathing losses
For"ing and Breathing )osses
E$# ;#&MB 0?This softare is a!aila"le for donload at .epa.#o!$ttn$chief$softare$tanks$inde%.html
orJing reathing
VOCs, C>
en!ene
;oluene
E en!ene
=ylenes
n9he'ane
+,+, 9 ;rimethylpentane
#ny #dditional "#$ (if applicale):
5sing &K* !NJS ;.2 Softare to calculate For"ing and Breathing losses
This softare can "e purchased from .#lo"al.ihs.com
Component Controlled Emissions Nton4yr
VOCs, C>
en!ene;oluene
E en!ene
=ylenes
n9C8
++;rimethylp
?-t is possile to create a mi'ture in the E$# ;#&MB program similar to the composition of the produced*ater stored in the tanJs (eg, a mi'ture of . *ater and 1. condensate) to determine the emissions
EP$ ;anJs (accounts for *orJing, reathing and flash losses)
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Notes:
$ &nter variables into blue bo%es
$ &missions ill be in green bo%es
sh losses.
lash losses !otal &missions
3irect @easurement of Emissions
$rocess Bimulator @odels
lash losses
VOCs, C> VOCs, C>
en!ene en!ene
;oluene ;oluene
E en!ene E en!ene
=ylenes =ylenes
n9he'ane n9C8
+,+, 9 ;rimethylpentane +,+, 9 ;rimethylpentane
#ny #dditional "#$ (if applicale): #ny #dditional "#$ (if appli
#nnual Emissions
VOCs, C>
en!ene;oluene
E en!ene
=ylenes
n9C8
+,+, 9 ;rimethylpentane
the gas4oil ratio (DO6) method
Vasue!9eggs correlation
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00000
00000
00000
00000
00000
00000
00000
cale):
00000
00000
00000
00000
tons per year
00000
0000000000
00000
00000
00000
00000
6eport VOC emissions on
$roduced ater ;anJ(s);a
6eport "#$ emissions on$roduced ater ;anJ(s)ta or "#$ speciation ta ifthe values are greater thanor eual to 01 tpy
6eport VOC emissions on$roduced ater ;anJ(s);a
6eport "#$ emissions on$roduced ater ;anJ(s)ta or "#$ speciation ta ifthe values are greater thanor eual to 01 tpy
tion
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!urbine &mission Calculations 0fueled by natural gas1
Barnett Shale *hase II Identification Information: $Input variables into the b
Company Name: Insert Company and/or site name here. $&missions ill be in the
!urbine -:
;urine rating (@@tu4hr):
Operating hours4year:
pollutant emission factor (l4@@tu)? tpy
VOC 000+1 0000
0+ 0000
? Emission actors from #$9+, Chapter , ;ales 191 and 19+a
Company's 5ni7ue IdentificationNumber:
&O=
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Non,lare Combustive Devices
Barnett Shale *hase II Identification Information:
Company Name: Insert Company and/or site name here.
+ther -:
(eneral Information &missi
Emission actors for aste Das Btream(s) (l4@@scf)
&O' 100
Ies
Emission actors for $ilot Btream (l4@@scf)
&O' 100
Ies
Emission actors for #dded uel Btream (l4@@scf)
&O' 100
/
Stream Information
Stream Sent to lare No. 9 < ; ? >
$ilot(s) e': oil tanJ e': *ater tanJ
$il t( ) il t J t t J
Company's 5ni7ueIdentification Number:
091 Fhat "ind of device isthisG &nter a shortdescription of the devicetype.
Emissio(l4@@s
0
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(+ 4ethod for &stimating lash &missions
Barnett Shale *hase II Identification Information:
Company Name: Insert Company and/or site name here.
!an"-:
$ &nter variables into
$ &missions ill be in
Das Oil 6atio: in standard cuic feet of flash gas per arrel (BC4l) of oil4condensate pro
arrels of Oil or Condensate per day:
!his information is based on an analysis submitted by the applicant. lash Das @
lash Das Bpeciation:
mole . *eight . ;otal
&itrogen +/01/ 0 23-V405
CO+ 00% 0 23-V405
"+B 0/1// 0 23-V405
methane (C1) 180+8 0 23-V405 VOC *
ethane (C+) 0080 0 23-V405 en!ene *eig
propane (C) 0%8+ 0 23-V405 ;oluene *eig
i9utane (C) %/1+++ 0 23-V405 Ethylen!ene *eig
n9utane (C) %/1+++ 0 23-V405 =ylene *eig
i9pentane (C%) )? 11+ 0 23-V405
nonane (C>)? 1+/+8 0 23-V405
decane (C10>)? 1++ 0 23-V405 Contaminant !
en!ene
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'ylenes (@, $, O) 10818 0 23-V405 ethylen!ene 23
undecanes (C11>)? 1%81 0 23-V405 'ylene 23
;O;#AB: 00000 0 23-V405 n9he'ane (C8) 23
? -f @ of heptanes plus is given, you can change the value in the tale aove
? -f the @ of the total sample is given, you can adFust the @ of heptanes> until the Klash Das @K value aove euals the value on the la rep
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o%es
bo%es
0
mitted:
0
23-V405
23-V405
23-V405
23-V405
23-V405
23-V405
6eport ;otal VOC emissions on theappropriate tanJ ta
Back to WorkbookTab.
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6eport "#$ emissions on theappropriate tanJ ta or "#$speciation ta if the values aregreater than or eual to 01 tpy
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&%ample irst page of a (I,()HCalc eport:
Controlled egenerator ith lash !an"
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Controlled egenerator &missions section e%ample:
lash (as &missions section e%ample:
5ncontrolled egenerator ith lash !an"
5ncontrolled egenerator &missions section e%ample:
6eport these emissions asthe uncontrolled4controlledregenerator emissions
;otal VOC is 1+/8 tpy forthis e'ample for the
uncontrolled 4controlledregenerator emissions
6eport these emissions as
the flash tanJ emissions
;otal VOC is 0018/ tpy forthe flash tanJ emissions forthis e'ample
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lash (as &missions section e%ample:
5ncontrolled egenerator ith lash !an" ith recycle/recompression option
5ncontrolled egenerator &missions section e%ample:
6eport these emissions asthe Kuncontrolled4controlledregenerator emissionsK
;otal VOC is +1+%1 tpy forthis e'ample for theuncontrolled 4controlledregenerator emissions
6eport these emissions asthe flash tanJ emissions
;otal VOC is 0018/ tpy forthe flash tanJ emissions forthis e'ample
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lash (as &missions section e%ample:
6eport these emissions asthe Kuncontrolled4controlledregenerator emissionsK
;otal VOC is +1+%1 tpy forthis e'ample for theuncontrolled 4controlledregenerator emissions
&o emissions to report for flashtanJ that isrecycled4recompressed Ioumay leave this section lanJ orenter !eros
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Back to Glycol Dehydrator Tab.
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Back to Glycol Dehydrator Tab.
Back to Glycol Dehydrator Tab.
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Back to Glycol Dehydrator Tab.
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&K* !an" &%ample
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AooJ for the KCalculation 6esultsK Bection ofthe EP$ ;anJ printout for emissions data
rom the KControlled Nton4yrK column, readthe VOCs, C> emissions ;his is your;otal VOC emissions (or this e'ample
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-C Engines Aist of ;ypes
+ BtroJe Aean
BtroJe Aean
BtroJe 6ich
+ BtroJe Aean BtroJe Aean BtroJe 6ich
&o' (0910%. Aoad) 1< 0/ ++1
&o' (W0. Aoad) 1 0/< ++<
CO (0910% Aoad) 0/8 01<
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luorene 1
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O-AE6
&O= CO
)arge Fall ired 0922 44Btu/hr1 , 100 /
)arge Fall ired 0922 44Btu/hr1 , 10 /
)arge Fall ired 0922 44Btu/hr1 , 10 /
)arge Fall ired 0922 44Btu/hr1 , +/0 /
esidential urnaces , 0 2.1 5nco 0Small Boilers 0922 44Btu/hr1 , Co %0 /
Small Boilers 0922 44Btu/hr1 , Co + /
Small Boilers 0922 44Btu/hr1 , 5n 100 /
!angential ired Boilers 0ll1 , )o
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Caron ;etrachloride
Chloroen!e
Chloroform
Chrysene
Cyclohe'ane
cyclopentane
Ethylen!eneEthylene 3iromide
luoranthene
luorene
ormaldehyde +/0E90
-soutane
@ethanol
@ethylcyclohe'ane
@ethylene Chloride
n9"e'ane
n9&onane
n9Octane
n9$entane&aphthalene %0E90%
$henanthrene
$henol
$ropane
$yrene
Btyrene
;oluene
Vinyl Chloride
=ylene9u
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Distillate +il , Fater,Steam InTec)andfill (as , 5ncontrolled
+0E901 10E901
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+/0E90
%0E90%
110E90
10E90%
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Natural (as , )ean *remi% Natural (as , 5ncontrolled Natural (as , Fater,Steam InTection
0E90+ +0E901 10E901
1%0E90+ /+0E90+ 00E90+
0E90
+10E90 +10E90 +10E90
880E90 880E90 880E90
10E90 10E90 10E90
00E90% 00E90% 00E90%
80E908 80E908 80E908
1+0E90% 1+0E90% 1+0E90%
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+0E90% +0E90% +0E90%